Refrigeration



March 26, 1940.v w. G. KGEL rs1' AL REFRIGERAT'ION 193e 2 sheets-sheet 1 Filed Deo 3l RNEY.

March 26, 1940. w G, KGEL E1- AL 2,194,505 `REFRIGrsRATIoN Filed DBC. 3l, 1936 2 Sheets-Sheet 2 :1 *362 k l /7 L? f 4f v /ag I zri 3 6a u ff zo F ff HLW lNvENTOR WMMM BY 00% @mgm REIS'SEW.

Patented Mar. 26,1940 um y UNITED s'r'res PATENT, OFFICE 2,194,505 nEFmGERATloN Wilhelm Georg Kgel and Per Paul Strandberg,

Stockholm, Sweden, assignors, by mesne assignments, to Servel, Inc., New York, N. Y., a corporation of Delaware Application December 31, 1936, Serial No. 118,558 In Germany January 8, 1936 4 Claims. (Cl. (i2-119.5) My invention relates to refrigeration, and more derstood by reference to the following descripparticularly to absorption' refrigerating systems tion taken in connection with the accompanying of the kind containing an auxiliary agent or drawings of which Fig. 1 diagrammatically illuspressure equalizing gas. trates absorption refrigeration` apparatus of a In absorption refrigerating systems of this kind pressure equalized type embodying my invention; a liquid refrigerant or cooling agent, such as am- Fig. 2 is an enlarged fragmentary sectional view monia, evaporates and diffuses in an evaporator of the evaporator shown in Fig. 1 illustrating into an auxiliary agent or inert gas, such as more clearly one embodiment of my invention; hydrogen, with consequent absorption of heat Figs. 3 and 4 are sectional views of two modifica- 10 from the surroundings. The resulting gas mixtions of the embodiments shown in Figs. 1 and 2; 10 ture of ammonia and hydrogen ows from the and Figs. 5 and 6 are a side andend elevation, evaporator to an absorber in which the ammonia respectively, of a further modification of the inis absorbed into liquid absorbent such as water. vention.

15 The inert hydrogen gas is returned to the evap- 'Referring to Fig. l, I have shown the present 15 orator and the enriched absorption solution is improvement embodied in a type of absorption conducted to a generator. 4 By heating the generrefrigeration systemgenerally like that described ator the ammonia is expelled from the absorption in Patent No. 1,609,334 to von Platenv and Muntsolution, liqueed in a condenser, and then reers. The refrigerating system comprises a gen- 20 turned to the evaporator to complete the refrigerator 9 containing a refrigerant; such as. am-

erating cycle. The weakened absorption solumonia, in solution in a body of absorption liquid, 20 tion from which the ammonia has been expelled such as water. The generator 9 may be heated is conducted from the generator to the absorber in any suitable manner, as by a gas burner I0 to absorb ammonia gas. which is adapted to project its flame into the All of the liquid refrigerant supplied to -the lower end of a flue II. The heat applied to the 'evaporator does not always evaporate due to generator 9 and its contents expels the ammonia *25 variations in load on the evaporator, so that out of solution, and the ammonia vapor fiowsupover a period of time a quantity of unevaporated ward through the air-cooled rectifier I2 and a refrigerant passes through the evaporator. In liquid cooled rectifier I3 into the lower section accordance with my invention refrigerant that I4 of an air-cooled condenser. The ammonia does not evaporate in the evaporator at one time liquefied in the lower section I4 of the condenser is accumulated in such a manner that it is imfiows into the outer jacket of the rectifier I3. mediately available to produce useful refrigera- Water vapor is condensed in rectifiers I2 and I3 tion at another time.- I accomplish this by proand drains back to the generator 9. viding an evaporator which is so constructed and The liquefied ammonia flows from the rectifier arranged that the unevaporated refrigerant I3 through conduits I5 and I6 into the upper end 35 which would otherwise pass out of the evaporator of an evaporator section I1 into which is introis accumulated or stored in the lower part thereof. duced an auxiliary agent or inert gas, such as The accumulation of unevaporated refrigerant in hydrogen, from a conduit I8. The evaporator the evaporator is particularly advantageous in section I'I is of a coil type having disks o1' inserts that the refrigerant is immediately available for I9 which are provided with openings and ax- 40 quick freezing to hasten the production of ice ranged at spaced intervals therein so that shallow cubes or the like. In order that the refrigerat pools of liquid refrigerant are maintained in the ing system will operate at a relatively high efentire evaporator section, the refrigerant overficiency even when unevaporated refrigerant is flowing and dripping downward therein. The accumulated or stored in the lower part of the liquid ammonia evaporates and diffuses into the evaporator, the usual concentration of refriger-A hydrogen with consequent absorption' of heat ant in the system is preferably increased by an from the surroundings of the. evaporator section amount which is substantially proportional to I1, and the resulting rich gas mixture of amthe amount of refrigerant that can be accumumonia. and hydrogen flows from the evaporator 50 lated or stored. section I'I through the outer passage 20 of a gas The novel features which I believe to be charheat exchanger ZI and conduit 22 into the lower acteristic of my invention are set forth with parend of an air-cooled absorber 2-3. ticularity in the claims. The invention, both as The ammonia is absorbed out of the enriched to organization and method, together with obgas mixture into weak absorption liquid which 1 jects and advantages thereof, will be better unenters the` upper part of the absorber 23 from a consequent absorption of heat conduit 24. The hydrogen, which is practically insoluble and weak in ammonia, passes upwardly from the absorber 23 through a plurality of parallel tubes 25 which form the inner passage of the gas heat exchanger 2|, and conduit I8 into the upper end of the evaporator section I1.

The absorption liquid in the absorber 23 becomes enriched in ammonia and passes through the lower end of conduit 22 into'a vessel 26. From the vessel 26 the enriched absorption liquid ows `through the inner passage 42l of a liquid heat exchanger to a coil 28, and is raised by va.-

por-lift action through conduit 29 into the upper part of the generator 9. 'I'he absorption liquid weak in ammonia flows from the lower part of the generator through a conduit 30, outer passage 3| of the liquid heat exchanger, and conduit 24 into the upper end of the absorber 23.

When the temperature of the cooling air is not suiiiciently low to liquefy all of the ammonia vapor in the lower sectio I4 of the condenser, the ammonia. vapor flowing into the outer jacket of the liquid cooled rectifier I3 passes into the upper section 32 of the air-cooled condenser..

'I'he ammonia vapor liquefied in the upper section 32 ows through a conduit 33 into an upper evaporator section 34 which is connected by conduits 35 and 36 to the outer passage 20 of the gas heat exchanger 2|. Liquid ammonia evap.

crates and diffuses into the rich gas which circulates through the evaporator section 34 with from the liquid ammonia and the surroundings.

The evaporator section 34 may be employed for cooling a storage space 31 in which both sections ofy the evaporator are disposed, a plurality of fins 38 being provided? on the evaporator section 34 -to increase the effective heat transfer surface. 'I'l'ie liquid ammonia cooled in the evaporator section 30 flows through conduits I6 and I6 into the upper end of the evaporator section I1 which may be employed as a freezing unit.

Ihe lower end of the upper sectionv 32 of the condenser is connected Iby conduit 39, vessel 40, and conduit 4| to the gas circuit, so that any hydrogen which may pass through theV condenser can flow to the gas circuit and not be trapped in the condenser. Ammonia vapor not liquefied in the condenser will flow through conduit 39 to displace hydrogen in the vessel 40 and force such hydrogen through conduit 4| into the gas circuit, thereby raising the total pressure in the System so that an adequate condensing lpressure is obtained for the increased temperature of the condenser. f

In'accordance with my invention I provide a vessel 42 at the lower end of the evaporator section I1 toaccumulate unevaporated refrigerantv that passes through the latter. The vessel 42 actually forms a part of the evaporator section I 1" and is connected in series relation therewith.

'i'he lower end of the ycoil forming the evaporator sectionv |'I is'vconnected to one end of the vessel 42, and the other end of the vessel is connected by a conduit 43 to the outer passage of the gas heat exchanger 2|. The vessel 42 is provided with a plurality of spaced bafiles 44 which are considerably higher than the openings in the inserts or disks I9 in the evaporator section I1, adjacent ballies 44 having openings 45 at the upper'and lower parts thereof and in staggered relation, as shown most clearly in Fig. 2. To the left-hand end of the vessel 42 is connected an overow conduit 46 having its lower end connected to the bottom ofthe vessel and its upper end connected to the conduit 43 at approximately the same height as the upper openings in the baiiles 44. f

When` the refrigerating system is in operation, liquid refrigerant enters the upper part of the evaporator section II-through the conduit I6 and pools of refrigerant are formed in the evaporator due to the inserts I9. This liquid refrigerant evaporates and ldiffuses into the inert hydrogen gas whichvis introduced into the evaporator from the conduit I8. The gas mixture formed gradually becomes richer in ammonia and ows through conduit 43 into the gas heat exchanger 2|.

During voperation 'of the refrigerating system the variations in load on the evaporator section I1 may be such that attimes liquid ammonia evaporates at a rate which is less than the rat'e at which liquid ammonia is supplied to the evaporator section I1, and the unevaporated liquid ammonia ows into the right hand pocket or chamber of the vessel 42. If the vessel'42 should contain absorption solution, due to tipping of the apparatus during transportation, for example, the liquid ammonia settles on top of the absorption solution and presses the latter into the second pocket-or chamber through the opening 45 at the bottom of therst baie 44. This raises the level of absorptionsolution in the second pocket whereby the absorption solution flows through the successive pockets o'r chambers in i vessel 42 is purged of absorption solution and the relatively high ammonia dependent upon the emrefrigerant assumes a concentration which is ciency of the air-cooled and liquid-cooled recti-g fiers I2 and I3.

If, for instance, trays containing water to be frozen are inserted into the freezing unit, the load on the evaporator is temporarily increased Due to this temporary increase in load., more liquid ammonia can evaporate and diffuse into the inert hydrogen gas. By providing the vessel 42, liquid ammonia is immediately available in the freezing unit to take 'care yof the temporary increase in load, and the accumulated liquid ammonia evaporates and diffuses linto the inert hydrogen gas with consequent absorption of heat from the surroundings. Thus, the accumulation vessel 42 permits quick freezing in the evaporator The refrigerating system is charged withl a quantity of ammonia that .will permit the system to operate most eii'iciently under all operating conditions that Since liquid ammonia will accumulate in the-,vessel 42 overa period of time due to variations in load on the evaporator section I1, the concentration of ammonia in the absorption solution is gradually decreased. 1f a particular refrigerating system operates most efdciently in a normal operating range with a twenty-eight .per cent solution of ammonia, for example, the accumulation of ammonia in the vessel 42 will reduce and mechanical lifting Athe vessel 42 and overflows into the conduit 43 section I1 which is utilized yas the freezing unit.

are normally encountered.

Fig. 3v in that the time required to freeze water thegconcentration of ammonia and absorption .solution .considerably below twenty-eight per cent. -In order that the refrigerating system will operate efficiently when liquid ammonia is stored inthe vessel 42, the concentration of ammonia in .the absorption solution placed in 'the system is increased to a value which may be thirty-five per cent, for example. This increase in concentration of absorption solution is preferably such that, when the vessel 4,2 is filled with unevaporated ammonia, the average concentration of ammonia in the absorption liquid circuit of the system will be substantially equal to the concentration which would normally obtain if no accumulation vessel were provided., The size of the accumulation vessel 42 may be varied and should be made sufllciently large in any particular case to take care of any temporary increase in load whereby rapid withdrawal of heat can be immediately effected.

In Fig. 3 I have shown a modification of the embodiment illustrated in Fig. 1 in which quick freezing is accelerated considerably. Instead of introducing the weak gas into the upper end of the evaporator section. I1, and having the weak gas in parallel flow with liquid refrigerant, as in the embodiment just described, the modification in Fig. 3 is so constructed and arranged that the weak gas passes from the inner passage of the gas heat exchanger 2| through conduit |8a into the accumulation vessel 42 and flows upward in the evaporator section in counter-how to the liquid ammonia. The enriched gas mixture passes from the upper end of the evaporator section I1 through conduit 43a into the outer passage 20 of the gas heat exchanger, the overflow conduit 46a from the vessel 42 being connected to the conduit 43a.

By causing the weak gas from the gas lieat exchanger 2| to flow over the surface of the low temperature refrigerant in the accumulation vessel 42, the time required to freeze trays containing Water or the like is reduced considerably because the partial Vapor pressure of the ammonia f' in the weak gas is relatively low and the liquid refrigerant evaporates and diffuses into the gas at a low temperature with consequent absorption of heat from the surroundings. With this arrangement the gas flowing through the upper part of the evaporator section is richer in ammonia than in the embodiment shown in Fig. 1. However, this is counterbalanced to a great extent in that in Fig. 1 the warm gas from the gas heat exchanger 2| gives up its heat to the upper part `of the evaporator section whereas in the modification just described the gas flowing in the upper part of the evaporator section is rst cooled in the accumulation vessel 42. Y

In the modification shown in Fig. 4 the weak gas from the gas heat exchanger 2| ows through conduit |8b into the accumulation vessel 42. Instead of having the gas and liquid refrigerant in counter-flow in the evaporator -section |1, however, the gas mixture flows from the vessel 42 through conduit |8c into the upper end of the evaporator section I1 and is in parallel flow or flows in the same direction as the liquid ammonia. The unevaporated refrigerant flows from the lower part of the evaporator section I1 through conduit 41 into the lower end of the vessel 42 whichis slightly inclined to the horizontal, and the overflow conduit 48 is connected to the higher end of the vessel and to the conduit 43h.

The modification just described possesses the same advantages as the modification shown in l or the like in the freezing unit is reduced considerably. By passing the weak gas over the stored liquid ammonia the time required to produce ice cubes and the like has been reduced to as much as 45 per cent of the time required in an evaporator of an ordinary type in which no provision is made for storing unevaporated refrigerant in the evaporator.

One manner of carrying the present invention into practice is shown in Figs. 5 and 6. The upper evaporator section adapted to be used for space cooling comprises a pipe or conduit 34' provided with a plurality of cooling fins 38'. A plurality of inserts 49 may be disposed in the conduit 38 to increase the effective gas and liquid contact surface; `The lower evaporator section comprises a looped coil arranged in good thermal contact with plates 50 and 5| which form spaced shelves of a freezing unit. The longitudinal and rear edge portions of each pair of abutting plates 50 and 5| are bent about half the circumference of the -coil |1', and the bent tabs 52 provided along the longitudinal edge portions o1' the plates extend through openings or slots in vertical plates 53 `and 54 which form the side Walls of the freezing unit.

I'he accumulation vessel comprises a larger U- shaped conduit 42 which is provided with closed ends and arranged in good thermal contact with abutting plates 55 and 56 in the same mannerthat the coil I'l is arranged in thermal contact with the plates 50 and 5|. The conduit 42' is provided with bafiies 44' similar to the bames 44 in Fig. 2.

The lower end 51 of the evaporator coil il is connected to one end of the conduit 42 and the other end of this conduit is connected by the overflow conduit 58 to the outer passage of the gas heat exchanger 2|.

By providing the U-shaped conduit 42 as the vessel for accumulating unevaporated refrigerant passing through the evaporator coil a'relatively large quantity of liquid refrigerant caribe stored in the lower part of the freezing unit. Thus, when a tray containing ywater to be frozen is placed on the shelf formed by the plates 55 and 56, an extremely rapid withdrawal of heat is effected to provide quick freezing for the production of ice cubes.

Instead of providing a separate vessel for storing unevaporated refrigerant passing through the evaporator and utilizing the stored refrigerant `for useful refrigeration upon increase in load on the evaporator, the lower part of an evaporator may be provided with inserts of such height that the unevaporated refrigerant cannot pass out of the evaporator. When this is done, however, it is preferable to provide suitable means whereby absorption solution collected in the lower part of the evaporator can be removed therefrom and returned to the absorption solution circuit.

Although particular .embodiments of the invention have been shown and described, it will be apparent to those skilled in the art that modifications may be made without departing from the spirit and scope of the invention, as pointed out in the following claims.

tribute liquid refrigerant in the evaporator in a Y manner to provide large surface for surface evaporation relative to liquid quantity, means to flow condensate directly onto said distributing means,

' lateral dimensions as to hold a quantity of re- -frigerant having largevolume relative to surface area exposed to inert gas and of such volume as to cause an appreciable variation in concentration of absorption liquid .when its complement of refrigerant liquid is added to the absorption liquid in the system, said pocket being situated to receive residue unevaporated liquid flowing downwardly beyond said distributing means and disposed in heat exchange relation with the object to be refrigerated and so that liquid refrigerant in said pocket is in the presence of circulating inert gas.

2. In an absorption refrigeration system as set forth in claim 1, means in said pocket to expel absorption liquid therefrom.

3. In an absorption refrigeration system having a generator, condenser, absorber and evaporator interconnected for flow of refrigerant, absorption liquid and inert gas, means to cause distribution of liquid refrigerant in the evaporator in a manner toprovide large surface for surface evaporation relative to liquid quantity, means to flow liquid refrigerant to said evaporator, said evaporator being constructed and connected and said distributing means being disposed for gravity ow of liquid refrigerant in a downward path, and structure providing a pocket of such size and shape as to hold a quantity of liquid refrigerant in the presence of circulating inert gas and of such volume as to cause an appreciable variation in concentration of absorption liquid when its complement of refrigerant liquid is added to the absorption liquid in the system, said pocket being connected to the end of said evaporator toward which liquid refrigerant flows past said distributing means and connected to receive liquid refrigerant beyond said distributing means and disposed in heat exchange relation with the objectvto be refrigerated, and said distributing means being disposed over a preponderantly major portion of the path of ow of liquid refrigerant provided by said pocket and the portion over which said distributing means extends, and Imeans in said pocket to expel absorption liquid therefrom.

4. An absorption refrigeration system as set yforth in claim 1, in which said evaporator is in the form of a pipe coil.v

WILHELM GEORG KOGEL.

PER PAUL 'STRANDBERG. 

